US20170283969A1 - Feeding systems and methods of using feeding systems - Google Patents
Feeding systems and methods of using feeding systems Download PDFInfo
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- US20170283969A1 US20170283969A1 US15/475,018 US201715475018A US2017283969A1 US 20170283969 A1 US20170283969 A1 US 20170283969A1 US 201715475018 A US201715475018 A US 201715475018A US 2017283969 A1 US2017283969 A1 US 2017283969A1
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- feed material
- chamber
- distribution unit
- gas
- feed
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- 239000000463 material Substances 0.000 claims abstract description 181
- 238000009826 distribution Methods 0.000 claims abstract description 86
- 238000003723 Smelting Methods 0.000 claims description 44
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims description 31
- 239000004744 fabric Substances 0.000 claims description 30
- 238000005243 fluidization Methods 0.000 claims description 25
- 238000001914 filtration Methods 0.000 claims description 16
- 239000000428 dust Substances 0.000 claims description 15
- 238000007599 discharging Methods 0.000 claims description 8
- 239000002245 particle Substances 0.000 claims description 5
- 239000007789 gas Substances 0.000 description 69
- 238000004891 communication Methods 0.000 description 10
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 7
- 229910052782 aluminium Inorganic materials 0.000 description 6
- 239000003517 fume Substances 0.000 description 4
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- 229910052751 metal Inorganic materials 0.000 description 4
- 239000002184 metal Substances 0.000 description 4
- 230000008569 process Effects 0.000 description 3
- 238000003860 storage Methods 0.000 description 3
- 238000005273 aeration Methods 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 238000007872 degassing Methods 0.000 description 2
- 238000005868 electrolysis reaction Methods 0.000 description 2
- 239000003792 electrolyte Substances 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
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- 229910000838 Al alloy Inorganic materials 0.000 description 1
- KLZUFWVZNOTSEM-UHFFFAOYSA-K Aluminum fluoride Inorganic materials F[Al](F)F KLZUFWVZNOTSEM-UHFFFAOYSA-K 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
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- 229910000831 Steel Inorganic materials 0.000 description 1
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Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65G—TRANSPORT OR STORAGE DEVICES, e.g. CONVEYORS FOR LOADING OR TIPPING, SHOP CONVEYOR SYSTEMS OR PNEUMATIC TUBE CONVEYORS
- B65G53/00—Conveying materials in bulk through troughs, pipes or tubes by floating the materials or by flow of gas, liquid or foam
- B65G53/34—Details
- B65G53/66—Use of indicator or control devices, e.g. for controlling gas pressure, for controlling proportions of material and gas, for indicating or preventing jamming of material
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65G—TRANSPORT OR STORAGE DEVICES, e.g. CONVEYORS FOR LOADING OR TIPPING, SHOP CONVEYOR SYSTEMS OR PNEUMATIC TUBE CONVEYORS
- B65G53/00—Conveying materials in bulk through troughs, pipes or tubes by floating the materials or by flow of gas, liquid or foam
- B65G53/04—Conveying materials in bulk pneumatically through pipes or tubes; Air slides
- B65G53/16—Gas pressure systems operating with fluidisation of the materials
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65G—TRANSPORT OR STORAGE DEVICES, e.g. CONVEYORS FOR LOADING OR TIPPING, SHOP CONVEYOR SYSTEMS OR PNEUMATIC TUBE CONVEYORS
- B65G53/00—Conveying materials in bulk through troughs, pipes or tubes by floating the materials or by flow of gas, liquid or foam
- B65G53/04—Conveying materials in bulk pneumatically through pipes or tubes; Air slides
- B65G53/16—Gas pressure systems operating with fluidisation of the materials
- B65G53/18—Gas pressure systems operating with fluidisation of the materials through a porous wall
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65G—TRANSPORT OR STORAGE DEVICES, e.g. CONVEYORS FOR LOADING OR TIPPING, SHOP CONVEYOR SYSTEMS OR PNEUMATIC TUBE CONVEYORS
- B65G53/00—Conveying materials in bulk through troughs, pipes or tubes by floating the materials or by flow of gas, liquid or foam
- B65G53/04—Conveying materials in bulk pneumatically through pipes or tubes; Air slides
- B65G53/16—Gas pressure systems operating with fluidisation of the materials
- B65G53/18—Gas pressure systems operating with fluidisation of the materials through a porous wall
- B65G53/22—Gas pressure systems operating with fluidisation of the materials through a porous wall the systems comprising a reservoir, e.g. a bunker
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65G—TRANSPORT OR STORAGE DEVICES, e.g. CONVEYORS FOR LOADING OR TIPPING, SHOP CONVEYOR SYSTEMS OR PNEUMATIC TUBE CONVEYORS
- B65G53/00—Conveying materials in bulk through troughs, pipes or tubes by floating the materials or by flow of gas, liquid or foam
- B65G53/34—Details
- B65G53/36—Arrangements of containers
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25C—PROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY OR REFINING OF METALS; APPARATUS THEREFOR
- C25C3/00—Electrolytic production, recovery or refining of metals by electrolysis of melts
- C25C3/06—Electrolytic production, recovery or refining of metals by electrolysis of melts of aluminium
- C25C3/14—Devices for feeding or crust breaking
Definitions
- the present patent application relates to a feeding system and methods of using a feeding system for feeding alumina into a smelting cell.
- Hall-Héroult electrolytic cells are utilized to produce aluminum metal in commercial production of aluminum from alumina that is dissolved in molten electrolyte (a cryolite “bath”) and reduced by a DC electric current using a consumable carbon anode.
- molten electrolyte a cryolite “bath”
- Traditional Hall-Héroult electrolytic cells require only a few feed points per cell.
- the present disclosure is generally directed towards feed systems and related methods of use, where the feed system is configured with a gas supply, where the gas supply and system components are configured to cooperate to fluidize a feed material into a fluidized feed material, which is then directed via the feed system components and devices (detailed herein) to provide a tailored delivery of feed material (e.g. amount, rate, intensity) to different locations in an end use application (e.g. container, reactor, electrolysis cell, or other industrial applications).
- an end use application e.g. container, reactor, electrolysis cell, or other industrial applications.
- the disclosure is configured to current and future electrolytic cell technology which may seek to feed small amounts of alumina in non-traditional cells at numerous points (e.g. 20 to 100 or more feed points per cell) depending on the physical size of the cell.
- non-traditional smelting cells using oxygen evolving anodes e.g. inert anode technology
- a feed system for distributing fluidized feed material comprises: a distribution unit configured to fluidize feed material; and a control unit fluidly coupled to the distribution unit, wherein the control unit comprises: a chamber configured to hold the feed material provided from the distribution unit; and a feeder unit fluidly coupled to the chamber: and a second gas inlet configured to provide gas to the chamber; and a material discharge pipe fluidly coupled to the chamber and the second gas inlet.
- the feed material is alumina.
- the feed material is configured to be fluidized with gas.
- the feed material is configured with properties and/or characteristics (e.g. average particle size, morphology, density, and/or composition) such that fluidization with a gas (e.g. air) to provide a flowable medium is achievable.
- properties and/or characteristics e.g. average particle size, morphology, density, and/or composition
- the distribution unit comprises: a body having a first volume; and a first chamber, within the first volume, at a bottom of the body, wherein the first chamber is configured to distribute gas (e.g. air) to the feed material within the first volume; and a second chamber within the first volume and above the first chamber, wherein the second chamber is configured to hold the feed material.
- the first volume is an area where fluidized material is flowing.
- the distribution unit comprises: a first fluidization fabric between the first chamber and the second chamber, wherein the feed material rests atop the fluidization fabric.
- the distribution unit further comprises: a feed material inlet pipe fluidly coupled to the first volume, wherein the feed material inlet pipe is configured to supply the feed material to the second chamber.
- the distribution unit further comprises: a pressure port, wherein the pressure port is configured to measure a depth of the feed material.
- the distribution unit further comprises: a first gas (e.g. air) inlet in the body, wherein the gas (e.g. air) inlet is configured to supply a gas (e.g. air) flow to the first chamber.
- a first gas e.g. air
- the gas e.g. air
- a gas e.g. air
- the distribution unit further comprises: a filtration fabric within the first volume, wherein the filtration fabric is disposed above the second channel.
- the distribution unit further comprises: a vent at a top of the body.
- control unit comprises: a fourth chamber configured to hold the feed material provided from the distribution unit; and a feeder unit fluidly coupled to the fourth chamber.
- the feeder unit comprises: a second gas (e.g. air) inlet configured to provide gas (e.g. air) to the fourth chamber; and a material discharge pipe fluidly coupled to the fourth chamber and the inlet.
- a second gas e.g. air
- gas e.g. air
- the feeder unit comprises: a point of entry device configured to break a crust formed at an opening of the smelting cell.
- the disclosed subject matter relates to a method of feeding a smelting cell, comprising: providing a feed material to a distribution unit, flowing gas (e.g. air) through the distribution unit, wherein the gas (e.g. air) fluidizes the feed material; and flowing a controlled amount of fluidized feed material from the distribution unit to a smelting cell via a control unit.
- gas e.g. air
- the feed material is alumina.
- flowing the controlled amount of fluidized feed material comprises: flowing the fluidized feed material to a control unit comprising: a chamber configured to hold the feed material provided from the distribution unit; and a feeder unit fluidly coupled to the chamber, wherein the feed material is configured to be de-fluidized in the chamber.
- gas e.g. air
- the feeder unit to fluidize the feed material in the chamber.
- the fluidized feed material is discharged from a discharge spout in the feeder unit to the smelting cell.
- a plunger prior to discharging the fluidized feed material, is extended to form an opening in a crust formed at an opening of the smelting cell to allow feed material to enter the smelting cell.
- flowing gas (e.g. air) through the distribution unit further comprises: filtering the gas (e.g. air) from the distribution unit that passes through the feed material to remove feed material dust particles.
- the disclosed subject matter relates to a method of feeding alumina to a smelting cell, comprising: providing alumina to a distribution unit; flowing gas (e.g. air) through the distribution unit, wherein the gas (e.g. air) fluidizes the alumina; and flowing the fluidized alumina to a control unit comprising: a chamber configured to hold the alumina provided from the distribution unit, wherein the alumina is de-fluidized in the chamber, and a feeder unit fluidly coupled to the chamber; providing gas (e.g. air) for a first period of time to the feeder unit to fluidize the alumina in the chamber; and discharging a controlled amount of the fluidized alumina from a discharge spout in the feeder unit to the smelting cell.
- gas e.g. air
- the disclosed subject matter relates to a method of feeding feed material to a destination, comprising: providing feed material to a distribution unit; flowing gas (e.g. air) through the distribution unit, wherein the gas (e.g. air) fluidizes the feed material; and flowing the fluidized feed material to a control unit comprising: a feeder unit fluidly coupled to the distribution unit; providing gas (e.g. air) for a first period of time to the feeder unit to fluidize the feed material in the control unit; and discharging a controlled amount of the fluidized feed material from a discharge spout in the feeder unit to the smelting cell.
- gas e.g. air
- a control unit comprising: a feeder unit fluidly coupled to the distribution unit; providing gas (e.g. air) for a first period of time to the feeder unit to fluidize the feed material in the control unit; and discharging a controlled amount of the fluidized feed material from a discharge spout in the feeder unit to the smelting cell.
- FIG. 1 depicts a schematic top view of a feed system in operative communication with alumina ore storage in accordance with some embodiments of the present disclosure.
- FIG. 2 depicts a schematic plan view of a distribution unit in operative communication with multiple control units in accordance with some embodiments of the present disclosure.
- FIG. 3 depicts a schematic elevation view of a distribution unit in operative communication with multiple control units in accordance with some embodiments of the present disclosure.
- FIG. 4 depicts a schematic view of a distribution unit in operative communication with multiple control units in accordance with some embodiments of the present disclosure.
- FIG. 5 depicts a schematic cross-sectional view of a distribution unit in operative communication with a control unit in accordance with some embodiments of the present disclosure.
- FIG. 6 depicts a schematic cross-section view of the control unit in accordance with some embodiments of the present disclosure.
- FIG. 7A-7B depicts a schematic cross section view of a feeder unit having a point of entry device in accordance with some embodiments of the present disclosure.
- FIG. 8 depicts a schematic cross-section view of a distribution unit in operative communication with a control unit in accordance with some embodiments of the present disclosure
- FIG. 1 depicts a schematic top view of a feed system in accordance with some embodiments of the present disclosure.
- the feed system 100 is in operative communication with a feed material storage system 102 .
- the feed material is a solid material that fluidizes (i.e. behaves like a fluid) when subjected to low pressure gas (e.g. air).
- the feed material is alumina.
- the feed material is smelter grade alumina and/or fluoride laden reacted alumina that has already passed through fume treatment systems (e.g. commingled).
- the feed system is calibrated differently depending on the type of alumina that is used.
- aluminum fluoride can be added into the distributor units to blend it in with the feed material to the smelting cell.
- the feed system 100 is configured to provide feed material to one or more smelting cells 104 via one or more distribution units.
- the smelting cell 104 is a conventional Hall-Héroult electrolytic cell.
- the smelting cell 104 is an advanced electrolysis cell (e.g. smelter of a non-ferrous metals that include oxygen evolving anodes and/or inert anodes).
- the feed system 100 is configured to utilize fluidization principles and/or with hydraulic head principles to permit low velocity distribution of feed material to discreet feed points to and within a smelting cell.
- the distribution systems can carry feed material in limited length flat sections as well as on gradual downhill slopes similar to those used with gas (e.g. air) gravity conveyors.
- the feed system permits the discharge of feed material along the lengths of sloped portions of the feed system (e.g. without the use of diverter valves).
- the amount of feed material discharged to the smelting cells is controllable without the use of physical gates or weirs.
- the feed system is configured with no moving parts exposed to the feed material that would be subject to wear and/or could contribute or create attrition of the feed material.
- the feed intensity is adjustable while maintaining the same overall feed rate per feed point.
- waste heat from the smelting process is used to preheat alumina feed material to reduce the overall energy requirements of the smelting process.
- feed points can be removed from the feed circuit and/or isolated for maintenance, while nearby feed points remain fully functional and continue to feed material into the cell (continues to be operated along it operating parameters).
- the amount of feed per individual feed point can be set independent of adjacent feed points even while being supplied from the same distributor unit.
- the feed system 100 comprises one or more distribution units 106 .
- feed material is provided to each distribution unit 106 from an inlet pipe 108 that is in operative communication with another distribution unit 106 or the feed material storage system 102 .
- the distribution unit 106 provides feed material to the smelting cell through multiple feed points 110 .
- one or more control units are fluidly coupled to each distribution unit 106 .
- the control unit is configured to regulate an amount and/or feed material distributed to the smelting cell 104 from the distribution unit 106 .
- FIGS. 2-5 depict a schematic view of a distribution unit in operative communication with one or more control units in accordance with some embodiments of the present disclosure.
- the distribution unit 106 comprises a body 202 .
- the body 202 of the distribution unit 106 is made from a material with sufficient strength to support system components (e.g. metal, aluminum and/or aluminum alloys, steel, specialty metals and/or non-reactive with feed materials and/or fluidized feed material).
- the body 202 is hollow.
- the body 202 has a first volume 204 .
- the body 202 comprises a top wall, opposing sidewalls, and opposing endwalls to define the first volume 204 .
- the body 202 comprises a first chamber 206 under the first volume 204 , which is configured to distribute gas (e.g. air) to feed material within the first volume via an gas (e.g. air) permeable membrane (fluidizing fabric).
- the first volume an area where fluidized material is flowing.
- the first chamber 206 is an gas (e.g. air) plenum.
- a gas (e.g. air) plenum is an gas (e.g. air) filled chamber in a structure, which receives gas (e.g. air) for distribution, for example, from a blower or a fan.
- the body 202 further comprises a second chamber 208 within the first volume 204 and above the first chamber 206 , wherein the second chamber 208 is configured to hold feed material received from the inlet pipe 108 .
- the second chamber is a feed material plenum.
- a feed material plenum is a feed material filled chamber in a structure, which receives feed material for distribution.
- the body 202 further comprises a first fluidization fabric 210 .
- the first fluidization fabric 210 is disposed between the top of the first chamber 206 and the bottom of the second chamber 208 .
- the feed material in the second chamber 208 rests atop the first fluidization fabric 210 .
- the first fluidization fabric 210 is gas (e.g. air) permeable, allowing gas (e.g. air) from the first chamber 206 to pass through to the feed material in the second chamber 208 and fluidize the feed material.
- the first fluidization fabric 210 is not feed material permeable, and thus does not allow any, or substantially any feed material to pass from the second chamber 208 to the first chamber 206 . In some embodiments, the first fluidization fabric 210 extends the length and width of the chambers 206 , 208 . In some embodiments, the first fluidization fabric 210 is a commercially available gas (e.g. air) permeable membrane.
- gas e.g. air
- suitable fluidizing fabric is FLUITEX® E and EX type fluidizing fabrics manufactured by MÜHLEN SOHN.
- the feed material inlet pipe 108 is fluidly coupled to the first volume 204 of the distribution unit 106 to supply the feed material to the second chamber 208 .
- the feed material inlet pipe 108 is made from a metal and/or metal alloy (e.g. aluminum).
- the feed material inlet pipe 108 is located in a center of the distribution unit body, or at an end of the distribution unit body, or at other suitable locations of the distribution unit body.
- the distribution unit 106 may comprise one or more feed material inlet pipes 108 .
- the body 202 of the distribution unit 106 further comprises one or more pressure ports 212 .
- pressure ports 212 are used in the distributor units 106 to determine how deep the feed material is within the fluidization zone.
- the pressure ports 212 are either tubes or ports located just above the fluidization fabric and connected to electronic manometers that correlate fluid pressure with depth and send signals to control devices which are used to monitor the condition of the feed system and to determine when problems may be occurring so that corrective measures can be undertaken by the control system.
- pressure transmitters may be either locally mounted and/or remote.
- the body 202 of the distribution unit 106 further comprises one or more first gas (e.g. air) inlets 214 configured to supply gas (e.g. air) to the first chamber 206 .
- first gas (e.g. air) inlet 214 is fluidly coupled to the first chamber.
- gas (e.g. air) is supplied to the first gas (e.g. air) inlet 214 from a fan or a blower.
- the gas e.g. air
- the body 202 comprises a filtration system 216 to remove feed material dust particles from the gas (e.g. air).
- the filtration system 216 is a dust filtration fabric within the first volume 204 .
- the dust filtration fabric is disposed in a third chamber 218 above the second chamber 208 to filter dust from the gas (e.g. air) as it passes through the dust filtration fabric.
- the dust filtration fabric is a commercially available filtration fabric typical to that used in commercial dust collection units.
- the filtration system is a vent at the top of the body 202 .
- the third chamber 218 has a first width at a first end proximate the second chamber 208 which gradually expands to a second width at an opposing second end proximate the top of the body 202 . The second width is greater than the first width.
- FIGS. 2-5 depict a schematic view of a distribution unit in operative communication with one or more control units in accordance with some embodiments of the present disclosure.
- FIG. 6 depicts a schematic cross-section view of the control unit in accordance with some embodiments of the present disclosure.
- the control unit 220 comprises a fourth chamber 226 configured to hold the feed material provided from the distribution unit 106 .
- the fourth chamber is a degassing (e.g. de-aeration) chamber.
- the fourth chamber 226 is fluidly coupled to the second chamber 208 .
- the fourth chamber 226 is fluidly coupled to the second chamber 208 via tube 224 and discharge block 222 as shown in FIG. 5 . Fluidized feed material flows into the volume 226 where it is no longer in contact with gas (e.g. air) from the distribution unit 106 . Accordingly, the feed material may no longer be fluidized and may not behave as a liquid.
- gas e.g. air
- control unit 220 further comprises a feeder unit 228 fluidly coupled to the fourth chamber 226 .
- the feeder unit 228 comprises a second gas (e.g. air) inlet 230 .
- gas (e.g. air) supplied from the gas (e.g. air) inlet 230 passes through a second fluidization fabric 232 to a fifth chamber 234 .
- a material passageway 236 has a first end that is fluidly coupled to the fifth chamber and has a second end that is fluidly coupled to the fourth chamber 226 .
- gas (e.g. air) from the second gas e.g.
- a material discharge pipe 238 is fluidly coupled to the fifth chamber 234 .
- the fluidized feed material is discharged from the material discharge pipe 238 to a smelting cell 104 or to another distribution unit 106 .
- the degassing (e.g. de-aeration) chamber permits the fluidized incoming feed material from the distributor unit to potentially de-fluidize, thereby creating a constant head to the inlet of the feeder unit.
- the constant head to the inlet of the feeder unit is configured to eliminate the need for tight control of feed material depth within the distributor units and permits the feeder unit to quickly respond with feed material flow when needed.
- the internal portions of the feeder unit are arranged to permit the hydraulic pressure to immediately push material through the feeder unit as soon as the fluidization gas (e.g. air) is activated.
- the fluidization gas (e.g. air) to each feeder unit is controlled by a valve (e.g.
- feed material doses from the feeder unit can be as small as fractions of a gram with gas (e.g. air) on times as low as 0.05 seconds with multiple pulses of gas (e.g. air) per second.
- feed material doses can be several grams to hundreds of grams provided intermittently depending on the on-time of the solenoid valve.
- the amount of feed material provided to smelting cell is customizable to the size of the smelting cell as well as to the need to sometimes feed more or less feed material depending on the operational circumstances of the smelting cell.
- the fluidization pressure on the feeder units is the same as that required for the distributor units and can be supplied by the same gas (e.g. air) source.
- feeder unit sizes are variable and customizable.
- control unit 220 does not have a fourth chamber 226 .
- control unit 220 is fluidly coupled to the distribution unit 202 via tube 224 and discharge block 222 .
- the feeder unit 228 further comprises a point of entry device configured to break through process material that can clog the opening of the material discharge pipe 238 .
- point of entry device is configured to break through a crust formed at an opening of the smelting cell to allow feed material to enter the smelting cell.
- FIG. 7A-7B depicts a schematic of a feeder unit having a point of entry device in accordance with some embodiments of the present disclosure.
- a material discharge pipe 238 has a crust breaker for breaking through any crust or other obstruction that may form on the top of the electrolyte bath and prevent feed material from mixing in the liquid portion of the bath.
- the crust breaker is a piston 702 mounted to the opening of the material discharge pipe 238 .
- metered feed material travels through the material discharge pipe 238 immediately before it is injected into the cell at a feed point.
- the piston can be extended from the opening of the material discharge pipe 238 to break through obstructions in the bath.
- the material discharge pipe 238 when the piston is extended as depicted in FIG. 7B , the material discharge pipe 238 is open, allowing feed material to enter the cell at a feed point. In some embodiments, when the piston is retracted, as depicted in FIG. 7A , the material discharge pipe 238 is closed and feed material is prevented from entering the cell. In some embodiments, when the piston is retracted, feed material accumulates in the material discharge pipe 238 above the piston. In some embodiments, when the piston is retracted, the material discharge pipe 238 is sealed with respect to fumes from the bath, preventing the bath fumes from mixing with the feed material inside of the material discharge pipe 238 and clogging the material discharge pipe 238 .
- feed material when the piston is in a partially extended position, feed material is dispensed into a feed point of the cell, but the piston does not enter the bath. In some embodiments, when the piston is in a fully extended position, feed material is dispensed into a feed point of the cell and the piston enters the bath, breaking any obstructions on the bath at the feed point.
- the piston may travel a first distance to a fully extended position.
- the first distance is 3 to 12 inches, or 5 to 12 inches, or 7 to 12 inches, or 9 to 12 inches, or 11 to 12 inches, or 3 to 9 inches, or 3 to 7 inches, or 3 to 5 inches.
- the piston acts as a crust breaker, breaking up any crust or other obstruction blocking feed material from entering the liquid portion of the bath.
- the piston may travel a second distance (e.g. 0.1 to 3 inches) to a partially extended position.
- the second distance is 0.1 to 3 inches, or 1 to 3 inches, or 2 to 3 inches, or 0.1 to 2 inches, or 0.1 to 1 inches.
- the piston does not extend into the liquid portion of the bath.
- the material discharge pipe 238 is open, allowing feed material to exit the material discharge pipe 238 .
- the feed system 100 is constructed of aluminum with bolted designs that utilize helicoil inserts in the aluminum with shoulder bolts to maintain known sealing pressures and compression on the various fluidization fabrics used in the distributors and seal leg devices.
- the material component construction e.g. aluminum construction
- at least one section of the feed gas (e.g. air) gravity conveyor that is non-conductive (e.g. constructed out of fiberglass or similar composite material) to maintain electrical isolation between the smelting cell and adjacent building structures.
- the feed material distributor units can be about 0.5 inch wide to about 5 inches wide at the fluidization fabric surface depending on the amount of feed material that is to be distributed.
- the various fluidization fabrics described herein may have different characteristics within the feed system, such as rated permeability, thickness, ply, material, etc. depending on where and how they are used.
- fluidization fabrics used within the feed system can be employed with commercially available components.
- the gas (e.g. air) used for fluidization is filtered for particulate.
- the gas (e.g. air) used for fluidization can be generated by a centrifugal blower or a positive displacement blower.
- the gas (e.g. air) consumption for feed system described in this disclosure will be close to the minimum fluidization requirement of alumina (e.g. minimizing waste of gas). Accordingly, the amount of gas (e.g. air) to be filtered for dust after flowing through the feed material is minimal as well.
- localized filtration fabric may be used on special gas (e.g. air) release chambers equipped with automatic cleaning mechanisms to eliminate the need for external ducting and fans normally associated with dust collection systems.
- vent hoods are used to carry particulate laden gas (e.g. air) from the distribution units to either dust collection systems or to divert it back into the smelting cell enclosure where it mixes with the normal fume exhaust from the smelting cell.
- particulate laden gas e.g. air
- a method of feeding a smelting cell using embodiments of the feed system 100 described above includes: providing a feed material to a distribution unit, flowing gas (e.g. air) through the distribution unit, wherein the gas (e.g. air) fluidizes the feed material; and flowing a controlled amount of fluidized feed material from the distribution unit to a smelting cell via a control unit.
- gas e.g. air
- flowing a controlled amount of fluidized feed material comprises: flowing the fluidized feed material to a control unit as described above, wherein the feed material is de-fluidized in the control unit chamber (e.g. the fourth chamber 226 ).
- gas e.g. air
- the feeder unit for a first period of time, for example for at least about 0.5 seconds, to fluidize the feed material in the seal leg 228 and distribute a predetermined amount of feed material to the smelting cell.
- a method of feeding feed material to a destination comprises: providing feed material to a distribution unit; flowing gas (e.g. air) through the distribution unit, wherein the gas (e.g. air) fluidizes the feed material; and flowing the fluidized feed material to a control unit comprising: a feeder unit fluidly coupled to the distribution unit; providing gas (e.g. air) for a first period of time to the feeder unit to fluidize the feed material in the control unit; and discharging a controlled amount of the fluidized feed material from a discharge spout in the feeder unit to the smelting cell.
- gas e.g. air
- a control unit comprising: a feeder unit fluidly coupled to the distribution unit; providing gas (e.g. air) for a first period of time to the feeder unit to fluidize the feed material in the control unit; and discharging a controlled amount of the fluidized feed material from a discharge spout in the feeder unit to the smelting cell.
Abstract
Description
- This application is a non-provisional patent application of and claims priority to U.S. provisional patent application Ser. No. 62/315,430, filed Mar. 30, 2017, the entirety of which is hereby incorporated by reference.
- Broadly, the present patent application relates to a feeding system and methods of using a feeding system for feeding alumina into a smelting cell.
- Hall-Héroult electrolytic cells are utilized to produce aluminum metal in commercial production of aluminum from alumina that is dissolved in molten electrolyte (a cryolite “bath”) and reduced by a DC electric current using a consumable carbon anode. Traditional Hall-Héroult electrolytic cells require only a few feed points per cell.
- The present disclosure is generally directed towards feed systems and related methods of use, where the feed system is configured with a gas supply, where the gas supply and system components are configured to cooperate to fluidize a feed material into a fluidized feed material, which is then directed via the feed system components and devices (detailed herein) to provide a tailored delivery of feed material (e.g. amount, rate, intensity) to different locations in an end use application (e.g. container, reactor, electrolysis cell, or other industrial applications).
- In some embodiments, the disclosure is configured to current and future electrolytic cell technology which may seek to feed small amounts of alumina in non-traditional cells at numerous points (e.g. 20 to 100 or more feed points per cell) depending on the physical size of the cell. In some embodiments, non-traditional smelting cells using oxygen evolving anodes (e.g. inert anode technology) may be operated with close control of feed dispersion and/or the operating parameters of distributing and/or spreading the feed around the entire electrolytic cell while feeding near continuously.
- In one embodiment, a feed system for distributing fluidized feed material, comprises: a distribution unit configured to fluidize feed material; and a control unit fluidly coupled to the distribution unit, wherein the control unit comprises: a chamber configured to hold the feed material provided from the distribution unit; and a feeder unit fluidly coupled to the chamber: and a second gas inlet configured to provide gas to the chamber; and a material discharge pipe fluidly coupled to the chamber and the second gas inlet.
- In another embodiment, the feed material is alumina.
- In some embodiments, the feed material is configured to be fluidized with gas. In some embodiments, the feed material is configured with properties and/or characteristics (e.g. average particle size, morphology, density, and/or composition) such that fluidization with a gas (e.g. air) to provide a flowable medium is achievable.
- In another embodiment, the distribution unit comprises: a body having a first volume; and a first chamber, within the first volume, at a bottom of the body, wherein the first chamber is configured to distribute gas (e.g. air) to the feed material within the first volume; and a second chamber within the first volume and above the first chamber, wherein the second chamber is configured to hold the feed material. In some embodiments, the first volume is an area where fluidized material is flowing.
- In another embodiment, the distribution unit comprises: a first fluidization fabric between the first chamber and the second chamber, wherein the feed material rests atop the fluidization fabric.
- In another embodiment, the distribution unit further comprises: a feed material inlet pipe fluidly coupled to the first volume, wherein the feed material inlet pipe is configured to supply the feed material to the second chamber.
- In another embodiment, the distribution unit further comprises: a pressure port, wherein the pressure port is configured to measure a depth of the feed material.
- In another embodiment, the distribution unit further comprises: a first gas (e.g. air) inlet in the body, wherein the gas (e.g. air) inlet is configured to supply a gas (e.g. air) flow to the first chamber.
- In another embodiment, the distribution unit further comprises: a filtration fabric within the first volume, wherein the filtration fabric is disposed above the second channel.
- In another embodiment, the distribution unit further comprises: a vent at a top of the body.
- In another embodiment, the control unit comprises: a fourth chamber configured to hold the feed material provided from the distribution unit; and a feeder unit fluidly coupled to the fourth chamber.
- In another embodiment, the feeder unit comprises: a second gas (e.g. air) inlet configured to provide gas (e.g. air) to the fourth chamber; and a material discharge pipe fluidly coupled to the fourth chamber and the inlet.
- In another embodiment, the feeder unit comprises: a point of entry device configured to break a crust formed at an opening of the smelting cell.
- In one embodiment, the disclosed subject matter relates to a method of feeding a smelting cell, comprising: providing a feed material to a distribution unit, flowing gas (e.g. air) through the distribution unit, wherein the gas (e.g. air) fluidizes the feed material; and flowing a controlled amount of fluidized feed material from the distribution unit to a smelting cell via a control unit.
- In another embodiment, the feed material is alumina.
- In another embodiment, flowing the controlled amount of fluidized feed material comprises: flowing the fluidized feed material to a control unit comprising: a chamber configured to hold the feed material provided from the distribution unit; and a feeder unit fluidly coupled to the chamber, wherein the feed material is configured to be de-fluidized in the chamber.
- In another embodiment, gas (e.g. air) is provided for a first period of time to the feeder unit to fluidize the feed material in the chamber.
- In another embodiment, the fluidized feed material is discharged from a discharge spout in the feeder unit to the smelting cell.
- In another embodiment, prior to discharging the fluidized feed material, a plunger is extended to form an opening in a crust formed at an opening of the smelting cell to allow feed material to enter the smelting cell.
- In another embodiment, flowing gas (e.g. air) through the distribution unit further comprises: filtering the gas (e.g. air) from the distribution unit that passes through the feed material to remove feed material dust particles.
- In one embodiment, the disclosed subject matter relates to a method of feeding alumina to a smelting cell, comprising: providing alumina to a distribution unit; flowing gas (e.g. air) through the distribution unit, wherein the gas (e.g. air) fluidizes the alumina; and flowing the fluidized alumina to a control unit comprising: a chamber configured to hold the alumina provided from the distribution unit, wherein the alumina is de-fluidized in the chamber, and a feeder unit fluidly coupled to the chamber; providing gas (e.g. air) for a first period of time to the feeder unit to fluidize the alumina in the chamber; and discharging a controlled amount of the fluidized alumina from a discharge spout in the feeder unit to the smelting cell.
- In one embodiment, the disclosed subject matter relates to a method of feeding feed material to a destination, comprising: providing feed material to a distribution unit; flowing gas (e.g. air) through the distribution unit, wherein the gas (e.g. air) fluidizes the feed material; and flowing the fluidized feed material to a control unit comprising: a feeder unit fluidly coupled to the distribution unit; providing gas (e.g. air) for a first period of time to the feeder unit to fluidize the feed material in the control unit; and discharging a controlled amount of the fluidized feed material from a discharge spout in the feeder unit to the smelting cell.
- For a more complete understanding of the present disclosure, reference is made to the following detailed description of exemplary embodiments considered in conjunction with the accompanying drawings.
-
FIG. 1 depicts a schematic top view of a feed system in operative communication with alumina ore storage in accordance with some embodiments of the present disclosure. -
FIG. 2 depicts a schematic plan view of a distribution unit in operative communication with multiple control units in accordance with some embodiments of the present disclosure. -
FIG. 3 depicts a schematic elevation view of a distribution unit in operative communication with multiple control units in accordance with some embodiments of the present disclosure. -
FIG. 4 depicts a schematic view of a distribution unit in operative communication with multiple control units in accordance with some embodiments of the present disclosure. -
FIG. 5 depicts a schematic cross-sectional view of a distribution unit in operative communication with a control unit in accordance with some embodiments of the present disclosure. -
FIG. 6 depicts a schematic cross-section view of the control unit in accordance with some embodiments of the present disclosure. -
FIG. 7A-7B depicts a schematic cross section view of a feeder unit having a point of entry device in accordance with some embodiments of the present disclosure. -
FIG. 8 depicts a schematic cross-section view of a distribution unit in operative communication with a control unit in accordance with some embodiments of the present disclosure -
FIG. 1 depicts a schematic top view of a feed system in accordance with some embodiments of the present disclosure. Thefeed system 100 is in operative communication with a feedmaterial storage system 102. In some embodiments, the feed material is a solid material that fluidizes (i.e. behaves like a fluid) when subjected to low pressure gas (e.g. air). In some embodiments, the feed material is alumina. In some embodiments, the feed material is smelter grade alumina and/or fluoride laden reacted alumina that has already passed through fume treatment systems (e.g. commingled). In some embodiments, the feed system is calibrated differently depending on the type of alumina that is used. In some embodiments, aluminum fluoride can be added into the distributor units to blend it in with the feed material to the smelting cell. - The
feed system 100 is configured to provide feed material to one or more smeltingcells 104 via one or more distribution units. In some embodiments, thesmelting cell 104 is a conventional Hall-Héroult electrolytic cell. In some embodiments, thesmelting cell 104 is an advanced electrolysis cell (e.g. smelter of a non-ferrous metals that include oxygen evolving anodes and/or inert anodes). - Without being bound by a particular mechanism or theory, the
feed system 100 is configured to utilize fluidization principles and/or with hydraulic head principles to permit low velocity distribution of feed material to discreet feed points to and within a smelting cell. In some embodiments, the distribution systems can carry feed material in limited length flat sections as well as on gradual downhill slopes similar to those used with gas (e.g. air) gravity conveyors. In some embodiments, the feed system permits the discharge of feed material along the lengths of sloped portions of the feed system (e.g. without the use of diverter valves). Furthermore, the amount of feed material discharged to the smelting cells is controllable without the use of physical gates or weirs. In some embodiments, the feed system is configured with no moving parts exposed to the feed material that would be subject to wear and/or could contribute or create attrition of the feed material. - In some embodiments, the feed intensity is adjustable while maintaining the same overall feed rate per feed point. In some embodiments, waste heat from the smelting process is used to preheat alumina feed material to reduce the overall energy requirements of the smelting process. In some embodiments, there are multiple feed points along the perimeter of the cell. In some embodiments, feed points can be removed from the feed circuit and/or isolated for maintenance, while nearby feed points remain fully functional and continue to feed material into the cell (continues to be operated along it operating parameters). In some embodiments, the amount of feed per individual feed point can be set independent of adjacent feed points even while being supplied from the same distributor unit.
- In some embodiments, the
feed system 100 comprises one ormore distribution units 106. In some embodiments, feed material is provided to eachdistribution unit 106 from aninlet pipe 108 that is in operative communication with anotherdistribution unit 106 or the feedmaterial storage system 102. In some embodiments, thedistribution unit 106 provides feed material to the smelting cell through multiple feed points 110. - In some embodiments, one or more control units (not shown in
FIG. 1 ) are fluidly coupled to eachdistribution unit 106. The control unit is configured to regulate an amount and/or feed material distributed to thesmelting cell 104 from thedistribution unit 106. -
FIGS. 2-5 depict a schematic view of a distribution unit in operative communication with one or more control units in accordance with some embodiments of the present disclosure. In some embodiments, thedistribution unit 106 comprises abody 202. In some embodiments, thebody 202 of thedistribution unit 106 is made from a material with sufficient strength to support system components (e.g. metal, aluminum and/or aluminum alloys, steel, specialty metals and/or non-reactive with feed materials and/or fluidized feed material). In some embodiments, thebody 202 is hollow. In some embodiments, thebody 202 has afirst volume 204. In some embodiments, thebody 202 comprises a top wall, opposing sidewalls, and opposing endwalls to define thefirst volume 204. In some embodiments, thebody 202 comprises afirst chamber 206 under thefirst volume 204, which is configured to distribute gas (e.g. air) to feed material within the first volume via an gas (e.g. air) permeable membrane (fluidizing fabric). In some embodiments, the first volume an area where fluidized material is flowing. In some embodiments, thefirst chamber 206 is an gas (e.g. air) plenum. As used herein, a gas (e.g. air) plenum is an gas (e.g. air) filled chamber in a structure, which receives gas (e.g. air) for distribution, for example, from a blower or a fan. In some embodiments, thebody 202 further comprises asecond chamber 208 within thefirst volume 204 and above thefirst chamber 206, wherein thesecond chamber 208 is configured to hold feed material received from theinlet pipe 108. In some embodiments, the second chamber is a feed material plenum. As used herein, a feed material plenum is a feed material filled chamber in a structure, which receives feed material for distribution. - In some embodiments, the
body 202 further comprises afirst fluidization fabric 210. In some embodiments, thefirst fluidization fabric 210 is disposed between the top of thefirst chamber 206 and the bottom of thesecond chamber 208. In some embodiments, the feed material in thesecond chamber 208 rests atop thefirst fluidization fabric 210. In some embodiments, thefirst fluidization fabric 210 is gas (e.g. air) permeable, allowing gas (e.g. air) from thefirst chamber 206 to pass through to the feed material in thesecond chamber 208 and fluidize the feed material. In some embodiments, thefirst fluidization fabric 210 is not feed material permeable, and thus does not allow any, or substantially any feed material to pass from thesecond chamber 208 to thefirst chamber 206. In some embodiments, thefirst fluidization fabric 210 extends the length and width of thechambers first fluidization fabric 210 is a commercially available gas (e.g. air) permeable membrane. An example of suitable fluidizing fabric is FLUITEX® E and EX type fluidizing fabrics manufactured by MÜHLEN SOHN. - In some embodiments, the feed
material inlet pipe 108 is fluidly coupled to thefirst volume 204 of thedistribution unit 106 to supply the feed material to thesecond chamber 208. In some embodiments, the feedmaterial inlet pipe 108 is made from a metal and/or metal alloy (e.g. aluminum). In some embodiments, the feedmaterial inlet pipe 108 is located in a center of the distribution unit body, or at an end of the distribution unit body, or at other suitable locations of the distribution unit body. In some embodiments, thedistribution unit 106 may comprise one or more feedmaterial inlet pipes 108. - In some embodiments, the
body 202 of thedistribution unit 106 further comprises one ormore pressure ports 212. In some embodiments,pressure ports 212 are used in thedistributor units 106 to determine how deep the feed material is within the fluidization zone. In some embodiments, thepressure ports 212 are either tubes or ports located just above the fluidization fabric and connected to electronic manometers that correlate fluid pressure with depth and send signals to control devices which are used to monitor the condition of the feed system and to determine when problems may be occurring so that corrective measures can be undertaken by the control system. In some embodiments, pressure transmitters may be either locally mounted and/or remote. - In some embodiments, the
body 202 of thedistribution unit 106 further comprises one or more first gas (e.g. air)inlets 214 configured to supply gas (e.g. air) to thefirst chamber 206. In some embodiments, the first gas (e.g. air)inlet 214 is fluidly coupled to the first chamber. In some embodiments, gas (e.g. air) is supplied to the first gas (e.g. air)inlet 214 from a fan or a blower. - In some embodiments, as gas (e.g. air) from the
first chamber 206 passes through the feed material in thesecond chamber 208 and fluidizes the feed material in the second chamber, the gas (e.g. air) can contain feed material dust particles. In some embodiments, thebody 202 comprises afiltration system 216 to remove feed material dust particles from the gas (e.g. air). In some embodiments, thefiltration system 216 is a dust filtration fabric within thefirst volume 204. In some embodiments, the dust filtration fabric is disposed in athird chamber 218 above thesecond chamber 208 to filter dust from the gas (e.g. air) as it passes through the dust filtration fabric. In some embodiments, the dust filtration fabric is a commercially available filtration fabric typical to that used in commercial dust collection units. In some embodiments, the filtration system is a vent at the top of thebody 202. In some embodiments, thethird chamber 218 has a first width at a first end proximate thesecond chamber 208 which gradually expands to a second width at an opposing second end proximate the top of thebody 202. The second width is greater than the first width. -
FIGS. 2-5 depict a schematic view of a distribution unit in operative communication with one or more control units in accordance with some embodiments of the present disclosure.FIG. 6 depicts a schematic cross-section view of the control unit in accordance with some embodiments of the present disclosure. In some embodiments, thecontrol unit 220 comprises afourth chamber 226 configured to hold the feed material provided from thedistribution unit 106. In some embodiments, the fourth chamber is a degassing (e.g. de-aeration) chamber. In some embodiments, thefourth chamber 226 is fluidly coupled to thesecond chamber 208. In some embodiments, thefourth chamber 226 is fluidly coupled to thesecond chamber 208 viatube 224 and discharge block 222 as shown inFIG. 5 . Fluidized feed material flows into thevolume 226 where it is no longer in contact with gas (e.g. air) from thedistribution unit 106. Accordingly, the feed material may no longer be fluidized and may not behave as a liquid. - In some embodiments, the
control unit 220 further comprises afeeder unit 228 fluidly coupled to thefourth chamber 226. In some embodiments, thefeeder unit 228 comprises a second gas (e.g. air)inlet 230. In some embodiments, gas (e.g. air) supplied from the gas (e.g. air)inlet 230 passes through asecond fluidization fabric 232 to afifth chamber 234. In some embodiments, amaterial passageway 236 has a first end that is fluidly coupled to the fifth chamber and has a second end that is fluidly coupled to thefourth chamber 226. In some embodiments, gas (e.g. air) from the second gas (e.g. air) inlet contacts the feed material in thefifth chamber 234 and fluidizes the feed material. In some embodiments, amaterial discharge pipe 238 is fluidly coupled to thefifth chamber 234. In some embodiments, the fluidized feed material is discharged from thematerial discharge pipe 238 to asmelting cell 104 or to anotherdistribution unit 106. - In some embodiments, the degassing (e.g. de-aeration) chamber permits the fluidized incoming feed material from the distributor unit to potentially de-fluidize, thereby creating a constant head to the inlet of the feeder unit. In some embodiments, the constant head to the inlet of the feeder unit is configured to eliminate the need for tight control of feed material depth within the distributor units and permits the feeder unit to quickly respond with feed material flow when needed. In some embodiments, the internal portions of the feeder unit are arranged to permit the hydraulic pressure to immediately push material through the feeder unit as soon as the fluidization gas (e.g. air) is activated. In some embodiments, the fluidization gas (e.g. air) to each feeder unit is controlled by a valve (e.g. normally closed solenoid valve operating on 24 VDC; which can be directly interfaced with a PLC controller). In some embodiments, feed material doses from the feeder unit can be as small as fractions of a gram with gas (e.g. air) on times as low as 0.05 seconds with multiple pulses of gas (e.g. air) per second. In some embodiments, feed material doses can be several grams to hundreds of grams provided intermittently depending on the on-time of the solenoid valve. In some embodiments, the amount of feed material provided to smelting cell is customizable to the size of the smelting cell as well as to the need to sometimes feed more or less feed material depending on the operational circumstances of the smelting cell. In some embodiments, the fluidization pressure on the feeder units is the same as that required for the distributor units and can be supplied by the same gas (e.g. air) source. In some embodiments, feeder unit sizes are variable and customizable.
- In some embodiments, as depicted in
FIG. 8 , thecontrol unit 220 does not have afourth chamber 226. In some embodiments, as depicted inFIG. 9 , thecontrol unit 220 is fluidly coupled to thedistribution unit 202 viatube 224 anddischarge block 222. - In some embodiments, the
feeder unit 228 further comprises a point of entry device configured to break through process material that can clog the opening of thematerial discharge pipe 238. In some embodiments, point of entry device is configured to break through a crust formed at an opening of the smelting cell to allow feed material to enter the smelting cell. -
FIG. 7A-7B depicts a schematic of a feeder unit having a point of entry device in accordance with some embodiments of the present disclosure. In some embodiments, amaterial discharge pipe 238 has a crust breaker for breaking through any crust or other obstruction that may form on the top of the electrolyte bath and prevent feed material from mixing in the liquid portion of the bath. In some embodiments, the crust breaker is apiston 702 mounted to the opening of thematerial discharge pipe 238. In some embodiments, metered feed material travels through thematerial discharge pipe 238 immediately before it is injected into the cell at a feed point. In some embodiments, the piston can be extended from the opening of thematerial discharge pipe 238 to break through obstructions in the bath. In some embodiments, when the piston is extended as depicted inFIG. 7B , thematerial discharge pipe 238 is open, allowing feed material to enter the cell at a feed point. In some embodiments, when the piston is retracted, as depicted inFIG. 7A , thematerial discharge pipe 238 is closed and feed material is prevented from entering the cell. In some embodiments, when the piston is retracted, feed material accumulates in thematerial discharge pipe 238 above the piston. In some embodiments, when the piston is retracted, thematerial discharge pipe 238 is sealed with respect to fumes from the bath, preventing the bath fumes from mixing with the feed material inside of thematerial discharge pipe 238 and clogging thematerial discharge pipe 238. In some embodiments, when the piston is in a partially extended position, feed material is dispensed into a feed point of the cell, but the piston does not enter the bath. In some embodiments, when the piston is in a fully extended position, feed material is dispensed into a feed point of the cell and the piston enters the bath, breaking any obstructions on the bath at the feed point. - In some embodiments, the piston may travel a first distance to a fully extended position. In some embodiments, the first distance is 3 to 12 inches, or 5 to 12 inches, or 7 to 12 inches, or 9 to 12 inches, or 11 to 12 inches, or 3 to 9 inches, or 3 to 7 inches, or 3 to 5 inches. In the fully extended position, the piston acts as a crust breaker, breaking up any crust or other obstruction blocking feed material from entering the liquid portion of the bath. In some embodiments, the piston may travel a second distance (e.g. 0.1 to 3 inches) to a partially extended position. In some embodiments, the second distance is 0.1 to 3 inches, or 1 to 3 inches, or 2 to 3 inches, or 0.1 to 2 inches, or 0.1 to 1 inches. In the partially extended position, the piston does not extend into the liquid portion of the bath. In some embodiments, in both the fully and partially extended positions, the
material discharge pipe 238 is open, allowing feed material to exit thematerial discharge pipe 238. - In some embodiments, the
feed system 100, except where otherwise noted, is constructed of aluminum with bolted designs that utilize helicoil inserts in the aluminum with shoulder bolts to maintain known sealing pressures and compression on the various fluidization fabrics used in the distributors and seal leg devices. In some embodiments, the material component construction (e.g. aluminum construction) results in a system that does not become magnetic around the smelting cells In some embodiments, at least one section of the feed gas (e.g. air) gravity conveyor that is non-conductive (e.g. constructed out of fiberglass or similar composite material) to maintain electrical isolation between the smelting cell and adjacent building structures. In some embodiments, the feed material distributor units can be about 0.5 inch wide to about 5 inches wide at the fluidization fabric surface depending on the amount of feed material that is to be distributed. - In some embodiments, the various fluidization fabrics described herein may have different characteristics within the feed system, such as rated permeability, thickness, ply, material, etc. depending on where and how they are used. In some embodiments, fluidization fabrics used within the feed system can be employed with commercially available components.
- In some embodiments, the gas (e.g. air) used for fluidization is filtered for particulate. In some embodiments, the gas (e.g. air) used for fluidization can be generated by a centrifugal blower or a positive displacement blower. In some embodiments, the gas (e.g. air) consumption for feed system described in this disclosure will be close to the minimum fluidization requirement of alumina (e.g. minimizing waste of gas). Accordingly, the amount of gas (e.g. air) to be filtered for dust after flowing through the feed material is minimal as well. In some embodiments, localized filtration fabric may be used on special gas (e.g. air) release chambers equipped with automatic cleaning mechanisms to eliminate the need for external ducting and fans normally associated with dust collection systems. In some embodiments, vent hoods are used to carry particulate laden gas (e.g. air) from the distribution units to either dust collection systems or to divert it back into the smelting cell enclosure where it mixes with the normal fume exhaust from the smelting cell.
- In some embodiments, a method of feeding a smelting cell using embodiments of the
feed system 100 described above, includes: providing a feed material to a distribution unit, flowing gas (e.g. air) through the distribution unit, wherein the gas (e.g. air) fluidizes the feed material; and flowing a controlled amount of fluidized feed material from the distribution unit to a smelting cell via a control unit. - In some embodiments, flowing a controlled amount of fluidized feed material comprises: flowing the fluidized feed material to a control unit as described above, wherein the feed material is de-fluidized in the control unit chamber (e.g. the fourth chamber 226). In some embodiments, gas (e.g. air) is provided to the feeder unit for a first period of time, for example for at least about 0.5 seconds, to fluidize the feed material in the
seal leg 228 and distribute a predetermined amount of feed material to the smelting cell. - In some embodiment, a method of feeding feed material to a destination, comprises: providing feed material to a distribution unit; flowing gas (e.g. air) through the distribution unit, wherein the gas (e.g. air) fluidizes the feed material; and flowing the fluidized feed material to a control unit comprising: a feeder unit fluidly coupled to the distribution unit; providing gas (e.g. air) for a first period of time to the feeder unit to fluidize the feed material in the control unit; and discharging a controlled amount of the fluidized feed material from a discharge spout in the feeder unit to the smelting cell.
- It will be understood that the embodiments described herein are merely exemplary and that a person skilled in the art may make many variations and modifications without departing from the spirit and scope of the disclosed subject matter. All such variations and modifications are intended to be included within the scope of the disclosure.
Claims (20)
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US20220186393A1 (en) * | 2019-03-20 | 2022-06-16 | Elysis Limited Partnership | System and method for collecting and pre-treating process gases generated by an electrolysis cell |
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- 2017-03-30 CN CN201780020748.XA patent/CN108883884B/en active Active
- 2017-03-30 CA CA3016442A patent/CA3016442C/en active Active
- 2017-03-30 US US15/475,018 patent/US10633752B2/en active Active
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EA201892210A1 (en) | 2019-02-28 |
WO2017173169A1 (en) | 2017-10-05 |
DK201870689A1 (en) | 2018-11-07 |
AU2017241823B2 (en) | 2019-11-14 |
US10633752B2 (en) | 2020-04-28 |
EP3436377A1 (en) | 2019-02-06 |
CA3016442C (en) | 2020-09-29 |
EA035849B1 (en) | 2020-08-20 |
CA3016442A1 (en) | 2017-10-05 |
DK180456B1 (en) | 2021-05-06 |
CN108883884B (en) | 2020-11-17 |
AU2017241823A1 (en) | 2018-09-20 |
BR112018069676A2 (en) | 2019-07-16 |
EP3436377A4 (en) | 2019-12-11 |
AU2019257382A1 (en) | 2019-11-14 |
CN108883884A (en) | 2018-11-23 |
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